几种硅藻土的表面电化学性质的研究

研究了浙江、吉林等地几种国内硅藻土的表面ζ电位与pH的关系曲线，测定了它们的等电点。其中吉林土等电点最小，表面酸强度最大。在所试条件下，浙江土和吉林土随着焙烧温度升高，等电点值增大，尿激酶吸附量随酸浓度增大而逐渐减小。而浙江土和酸洗浙江土在400℃时等电点最小，酸浓度最大，吉林土在400℃时比表面最大，三者对尿激酶吸附量也最大。酸洗后，浙江土等电点值增大，酸浓度则减小，尿激酶吸附量也相应减小。     

碳氟链与碳氢链表面活性剂在固液界面上的吸附

全氟辛酸及其钠盐和十二烷基硫酸钠在R972上的吸附等温线均为S型或LS型，指示固液界面吸附过程中有表面疏水缔合物生成．碳氟表面活性剂的饱和吸附量显著高于碳氢表面活性剂的饱和吸附量．加电解质于液相使各体系吸附量上升．对于碳氟表面活性剂，甚至引起吸附等温线类型变化．例如，不加电解质时全氟辛酸在R972上的吸附等温线为S型，而加入HCl（c＝0．05mol·dm－3）使吸附等混线变成LS型．全氟辛酸比全氟辛酸钠在R972上的吸附更强．几种表面活性剂在R972上的吸附均随温度升高而减少。应用两阶段吸附模型及通用吸附等温线公式可以很好地解释所得实验结果．     

活性炭纤维的微孔结构水吸附

测定了两种活性炭纤维（ACF）的氮气、水吸附等温线和XPS,研究了ACF的微孔结构和表面性质,用αs图分析氮吸附等温线获得了ACF的比表面积、微孔容量和微孔径。XPS表明在ACF表面存在多种不同结合状态的氧。水在ACF上的吸附等温线呈V型,具有很大的脱附滞后环。水通过与ACF表面的氧形成氢键发生吸附。ACF表面的初始吸附点多,则在低、中压时的水吸附量就大。     

氨基酸在固／水界面的吸附作用

本文研究了活性炭、硅胶和氧化铝自水中吸附酪氨酸和苯丙氨酸。所得的结构表明,（1）在活性炭/水界面上两种氨基酸的吸附等温线均为Langmuir型。极限吸附量nm^S、吸附常数b与介质pH值关系曲线大约在氨基酸等电点处有最大值,这可用介质pH对氨基酸溶解度的影响解释。在活性炭表面,氨基酸主要以两性离子躺方式吸附。（2）在硅胶（氧化铝）/水界面上的吸附等温线为S型,吸附量仅为在活性炭/水界面上的1‰,在硅胶表面苯丙氨酸主要以电性作用吸附;在氧化铝表面酪氨酸以两性离子与表面形成氨键吸附。     

国产硅藻土结构的研究

系统地研究了硅藻土结构, 发现除浙江白土表面具有双生的硅羟基外, 其它只有连生的与孤立的硅羟基; 经IR谱证明, 其内部尚有Si-O与Al-O振动, 酸洗或焙烧都能使硅藻体的孔径、孔径分布和结构发生改变; 经焙烧后, 结构均发生改变, 其自由水消失, 束缚水逐渐减少; 焙烧达1150℃时, 原组成无定形二氧化硅则晶化为α-方石英, 除吉林土具有一级孔洞, 云南土具有三级孔洞外, 本文中其它硅藻土均有二级孔洞。     

凹凸棒土对戊醇异构体吸附分离性能的研究

采用十六烷基三甲基溴化铵和β-环糊精对凹凸棒土进行改性,研究了凹凸棒土对戊醇异构体的吸附行为。实验结果表明,相同条件下正戊醇在凹凸棒土上的吸附量大于2-甲基-丁醇。以环己烷为溶剂,十六烷基三甲基溴化铵改性后的凹凸棒土对戊醇异构体的吸附量较大,但吸附分离性能较差;而β-环糊精改性的凹凸棒土对戊醇异构体有较好的吸附分离性能,吸附选择性和分离因子分别为92.24和12.16。Langmuir方程拟合呈现出了良好的线性关系,戊醇异构体在凹凸棒土上的吸附等温线符合二级动力学方程模型。     

聚乙烯亚胺表面改性硅藻土及其对苯酚吸附特性的研究

使用紫外吸收光度法研究了硅藻土对聚乙烯亚胺(PEI)的等温吸附;采用浸渍法,用PEI对硅藻土进行了表面改性;使用4-氨基安替比林光度法研究了经PEI表面改性的硅藻土对苯酚的捕集行为.研究结果表明,凭借强烈的静电相互作用,表面带负电荷的硅藻土粉体对阳离子性大分子PEI具有很强的吸附能力,等温吸附满足Freundlich吸附方程;经PEI表面改性后,硅藻土粉体表面的电性发生了根本性改变,且等电点由pH=2.0移至pH=10.5;在中性溶液中,改性粉体通过氢键作用与静电相互作用的协同,对水溶液中的苯酚会产生很强的捕集作用,饱和吸附量可达92 mg/g;在酸性溶液中改性粉体通过氢键相互作用,对水溶液中的苯酚产生一定的吸附作用,但由于PEI分子链高度的质子化,氮原子对苯酚的氢键相互作用很弱,吸附量很低.     

氨基酸在固体表面的吸附*

介绍了氨基酸在固体表面吸附的常见吸附模式和吸附等温线类型。在常见的等温式中Sips等温式能处理液相中吸附质浓度从低到高、吸附剂表面从均匀到不均匀等各种情形下的固/液吸附体系,得到的等温线一般归属4类：S型、L型、H型和C型;总结和讨论了各吸附参数对氨基酸吸附的影响,具体考察了氨基酸种类、固体表面的性质、溶剂种类、介质的pH、介质离子强度和温度等因素对氨基酸吸附的影响,指出通过优化各吸附参数,可以调整氨基酸和固体吸附剂之间的静电吸引力或疏水作用,达到最好的吸附效果;对氨基酸的固体吸附剂进行了分类阐述。     

胶溶法制备镧-钡共稳定氧化铝的性能

以硝酸为胶溶剂, 两种拟薄水铝石为前驱体, 用胶溶法制备了镧-钡共稳定的氧化铝. 采用X 射线衍射(XRD)、表面分析仪(BET)、氨气程序升温脱附(NH3-TPD)和NO2程序升温脱附(NO2-TPD)技术对所制备的镧改性和镧钡共改性氧化铝的结构特性和表面性能进行了表征. XRD结果表明, 改性氧化铝在1273 K焙烧后均以γ-Al2O3相存在. 当BaO添加量达到14%(w)时, 有少量BaCO3生成. BET结果表明, 在1273 K下焙烧5 h后, 5%(w)La2O3稳定的氧化铝(Ba-0)和5%La2O3与8%BaO共同稳定的氧化铝(Ba-8)均具有较大的比表面积, 各种氧化铝的吸附等温线表明它们的孔形状均为狭缝型孔和瓶型孔, 孔径分布曲线表明, 仅有样品Ba-8的孔径分布较宽, 孔径为6-10 nm, 其它三种样品的孔径均集中在10 nm; NH3-TPD结果表明, 随着氧化钡添加量的逐渐增多, 氧化铝表面的酸量、酸强度逐步减少. NO2-TPD结果表明, 添加BaO后载体对NO2的吸附量增多, 随着BaO含量的增多, 体相Ba(NO3)2增多. 由于样品Ba-8同时具有很好的织构性质、适中的表面酸量和酸强度分布及NO2吸附脱附能力, 使得以它为载体的催化剂具有最好的催化性能,丙烷的起燃温度和完全转化温度分别为526 K和593 K.     

聚乙二醇、聚丙二醇和环氧乙烷-环氧丙烷嵌段共聚物在固液界面上的吸附——Ⅰ.活性炭/水界面

测定了25℃时活性炭自水溶液中吸附五种聚乙二醇(PEG)、一种聚丙二醇(PPG)和三种环氧乙烷(EO)-环氧丙烷(PO)嵌段共聚物的吸附等温线。结果表明,各等温线均为Langmuir型的,且在较低浓度时即可达极限吸附。当以g.g~(-1)表示吸附量时,各聚合物的极限吸附量相近。对于PEG系列和EO-PO嵌段共聚物系列,极限吸附时每个分子占据的面积与分子中所含EO数的关系为两条斜率相同的直线。由直线斜率和后一直线的截距可求得每个EO和PO所占的面积分别为26和2.9 nm~2。这些结果支持了分子以其EO和PO链节都平躺在表面上的吸附模型。     

改性硅藻土对富营养化水体中磷的吸附行为

以硅藻土原土为原料,通过碱洗及浸渍负载羟基氧化铁对其进行改性,利用SEM、XRD及物理吸附仪对改性硅藻土的形貌、比表面积等进行表征,并研究了改性硅藻土对富营养化水体中磷的吸附性能。结果表明,(1)改性后,硅藻土杂质元素减少,孔径明显增大,比表面积增大23倍,并有效负载了β-FeO(OH);(2)其对磷的吸附受温度及pH值的影响,温度越高,达到吸附平衡时间越短,吸附容量也越大;在pH值为4~11之间,吸附容量随pH的增大而减小;(3)拟二级反应动力学方程,能准确地描述改性硅藻土对磷的吸附,而粒内扩散,不是改性硅藻土对磷吸附的唯一控制步骤;(4)改性硅藻土在富营养化水体中对磷的吸附行为,符合Freundlich等温线方程,其吸附过程为物理吸附,吸附过程焓变(H)为39.949kJ/mol,各温度下的自由能变(G)均小于零,熵变(S)均为正值,该吸附过程是自发的吸热物理过程。     

Removal of uranium from aqueous solutions by diatomite (Kieselguhr)

In this study, the removal of uranium from aqueous solutions by diatomite earth (Kieselguhr) fine particules has been investigated. Diatomite earth is an important adsorbent material in chromatographic studies. Uranium adsorption capacity of four different types of diatomite was determined. The adsorption of uranium on the chosen diatomite sample was examined as a function of uranium concentration, solution pH, contact time and temperature. The adsorption of uranium on diatomite followed a Langmuir-type isotherm.     

Adsorption of Malachite Green by Diatomite: Equilibrium Isotherms and Kinetic Studies

The utilization of diatomite as potential adsorbent to remove malachite green (MG) from aqueous solution was developed. The characterization of the diatomite was evaluated by scanning electron microscope (SEM) and Brurauer Emmerr Teller (BET). The operating variables of pH, diatomite mass, initial MG concentration, and adsorption reaction time were studied. The equilibrium, kinetics, and thermodynamic parameters were investigated as well. It was found that the diatomite was composed of integral and almost circle sieve tray with lots of small pores on it, which afforded the diatomite high specific surface area of 46.09 m² g^?1. The optimum pH and reaction time were 7 and 90 minutes, respectively. The MG removal increased accordingly as the diatomite mass increased. The isotherm results showed that the equilibrium data were fitted to Langmuir model better, indicating the MG adsorption was better characterized by mono-layer. The maximum mono-layer capacity obtained from Langmuir was 23.64 mg g^?1 at 25°C. The kinetic studies indicated that experiment data followed pseudo-second-order model better. It also revealed that intraparticle diffusion was not the only rate-controlling step. The thermodynamic results concluded that the adsorption process was endothermic and more favorable at high temperature. Researches confirmed the applicability of diatomite as an efficient adsorbent and low-cost process to remove hazardous materials.     

Adsorption of Gossypol from Cottonseed Oil on Oxides

The adsorption of gossypol, a toxic pigment and the major colorant in cottonseed oil, has been studied, using silicas and aluminas of different surface areas and pore size distributions. Gossypol has a high affinity for alumina surface, the adsorption isotherm follows the Langmuir equation, and the maximum amount adsorbed is compatible with a monolayer of molecules on the surface; this is indicative of chemisorption. The affinity for a silica surface is much lower and the adsorption isotherm follows the Freundlich equation. The amount adsorbed is also influenced by the pore size distribution, the useful surface area being that developed by pores larger than 3 nm, i.e., 2 to 3 times the size of the adsorbate. Copyright 2000 Academic Press.     

重量法测定环戊烷在silicalite-1分子筛上的吸附特性

用智能重量分析技术 (IGA)研究了环戊烷在silicalite 1分子筛上的吸附特性。结果表明 ,随着温度的降低 ,环戊烷的吸附等温线从第一类型过渡为第四类型 ,在 2 5 4K和 2 74K温度下吸附等温线呈现滞后环 ,为第四类型 ,而吸附等温线在 30 4K、32 3K下为阶梯形 ,在 35 4K、42 3K温度下呈第一类型 ,其中 42 3K温度下的吸附等温线可准确的用Langmuir方程来描述。本文同时讨论了吸附质分子间以及吸附质和吸附剂间的相互作用、分子结构特性、分子筛对吸附质分子的空间位阻、分子筛的能量不均匀表面等对环戊烷在silicalite 1分子筛上吸附性能的影响     

Studies on the Physical Adsorption Equilibria of Gases on Porous Solids over a Wide Temperature Range Spanning the Critical Region—Adsorption on Microporous Activated Carbon

Adsorption equilibria of nitrogen and methane on microporous ( < 2 nm) activated carbon were measured for a wide temperature range (103‐298 K) spanning the critical region. Information relating to Henry constants, the isosteric heat of adsorption, and the amount of limiting adsorption were evaluated. All isotherms show type‐I features for both sub‐ and supercritical temperatures. A new isotherm equation and a consideration for the importance of the effect of the adsorbed phase volume allow this kind of isotherms to be modeled satisfactorily. The model parameter of the saturated amount of absolute adsorption (n⁰_t) equals the limiting adsorption amount (n^itm), leaving the physical meaning of the latter clarified, and the exponent parameter (q) proves to be an appropriate index of surface heterogeneity.     

Removal of Reactive Yellow 84 from aqueous solutions by adsorption onto hydroxyapatite

The adsorption of a reactive dye, Reactive Yellow 84, from aqueous solution onto synthesized hydroxyapatite was investigated. The experiments were carried out to investigate the factors that influence the dye uptake by the adsorbent, such as the contact time under agitation, absorbent dosage, initial dye concentration, temperature and pH of dye solution. The experimental results show that the amount of dye adsorbed increases with an increase in the amount of hydroxyapatite. The maximum adsorption occurred at the pH value of 5. The equilibrium uptake was increased with an increase in the initial dye concentration in solution. The experimental isotherm data were analyzed using Langmuir isotherm equation. The maximum monolayer adsorption capacity was 50.25 mg/g. The adsorption has a low temperature dependency and was endothermic in nature with an enthalpy of adsorption of 2.17 kJ mol⁻¹.     

The significance of a second adsorption phase with weakly adsorbed species for the calculation of the surface concentrations of a mixture: methanol–DME and methanol–ethene adsorption in SAPO-34

With the calorimetric (adsorption heat versus coverage) curve also measured together with the adsorption isotherm, the simultaneous use of both curves showed that there were two phases of adsorption in the adsorption of methanol, dimethyl ether, ethene and propane in SAPO-34. The dual-site Langmuir equation gave good fits to the adsorption data to support the interpretation that a second (type 2) adsorption phase occurred in the high-pressure region in addition to a first (type 1) adsorption phase on the acid sites at lower pressures. Adsorption experiments and calculations using binary gas mixtures showed that due to the existence of two types of adsorption, the multicomponent Langmuir isotherm equation (Langmuir competitive adsorption model) calculated incorrect surface concentrations when the concentrations were high. In contrast, the ideal adsorbed solution theory (IAST) calculated correct surface concentrations in the adsorption of mixtures.     

Effect of adsorption on the surface tensions of solid-fluid interfaces

A method is proposed for determining the surface tensions of a solid in contact with either a liquid or a vapor. Only an equilibrium adsorption isotherm at the solid-vapor interface needs to be added to Gibbsian thermodynamics to obtain the expressions for the solid-vapor and the solid-liquid surface tensions, gamma[1](SV) and gamma[1](SL), respectively. An equilibrium adsorption isotherm relation is formulated that has the essential property of not predicting an infinite amount adsorbed when the pressure is equal to the saturation-vapor pressure. Five different solid-vapor systems from the literature are examined, and found to be well described by the new isotherm relation. The surface-tension expressions obtained from the isotherm relation are examined by determining the surface tension of the solid in the absence of adsorption, gamma[1](S0), a material property of a solid surface. The value of gamma[1](S0) can be determined by adsorbing different vapors on the same solid, determining the isotherm parameters in each case, and then from the expression for gamma[1](SV) taking the limit of the pressure vanishing to determine gamma[1](S0). From previously reported measurements of benzene and of n-hexane adsorbing on graphitized carbon, the same value of gamma[1](S0) is obtained.